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Environmental Research
journal homepage: www.elsevier.com/locate/envres
Usefulness of toxicological validation of VOCs catalytic degradation by air-
liquid interface exposure system
Margueritta Al Zallouha, Yann Landkocz, Julien Brunet, Renaud Cousin, Eric Genty,
Dominique Courcot, Stéphane Siffert, Pirouz Shirali, Sylvain Billet
⁎
Unité de Chimie Environnementale et Interactions sur le Vivant EA4492, Université du Littoral Côte d′Opale, 189 A Avenue Maurice Schumann, 59140
Dunkerque, France
ARTICLE INFO
Keywords:
Catalytic oxidation
Air-liquid interface exposure
Toluene
Toxicological validation
By-products identification
ABSTRACT
Toluene is one of the most used Volatile Organic Compounds (VOCs) in the industry despite its major health
impacts. Catalytic oxidation represents an efficient remediation technique in order to reduce its emission
directly at the source, but it can release by-products. To complete the classical performance assessment using
dedicated analytical chemistry methods, we propose to perform an untargeted toxicological validation on two
efficient catalysts. Using biological system allows integrating synergy and antagonism in toxic effects of emitted
VOCs and by-products, often described in case of multi-exposure condition. Catalysts Pd/α-Al
2
O
3
and Pd/γ-
Al
2
O
3
developed for the oxidation of toluene were both coupled to a Vitrocell
®
Air-Liquid Interface (ALI) system,
for exposure of human A549 lung cells during 1 h to toluene or to catalysts exhaust before quantification of
xenobiotics metabolizing enzymes.
This study validated initially the Vitrocell
®
as an innovative, direct and dynamic model of ALI exposure in the
assessment of the performances of new catalysts, showing the presence of chemically undetected by-products.
The comparison of the two catalysts showed then that fewer organic compounds metabolizing genes were
induced by Pd/γ-Al
2
O
3
in comparison to Pd/α-Al
2
O
3
, suggesting that Pd/γ-Al
2
O
3
is more efficient for toluene
total oxidation from a toxicological point of view.
1. Introduction
Volatile Organic Compounds (VOCs) represent a variety of sub-
stances belonging to different chemical families (aromatic hydrocar-
bons, ketones, alcohols, alkanes, aldehydes, etc.) and known for being
important contributors to air pollution (Khan and Ghoshal, 2000).
Among the major VOCs, Benzene, Toluene, Ethylbenzene and Xylenes
(BTEX) have major and direct impact on human health. Toluene is
widely used in many industrial sectors where 32% of commercial
toluene enter in the process of benzene synthesis and 19% is used as
solvents with almost 90 kt/year as paint solvents in European Union
(Hansen et al., 2002). Toluene has a relatively well known toxicity with
the respiratory tract as major route of absorption. Limit values for
occupational exposure to toluene were established in France, in 2012,
with an exposure limit value of 20 ppm equivalent to 76.8 mg/m
3
for
8 h and 100 ppm (384 mg/m
3
) on a short-term (under 15 min). The
same values were set for the 8 h exposure in the USA since 2007 (INRS,
2012).
After absorption, toluene is primarily metabolized in the liver,
where 80% of the absorbed dose undergoes a chain of oxidation
reactions by the intervention of different enzymes which make the
molecule more hydrophilic and allow urine excretion of metabolites.
Between 10% and 20% of inhaled toluene are excreted in the expired
air with a half-life of about 25 min (Benoit et al., 1985). Toluene is
known for both acute and chronic toxic effects (Tormoehlen et al.,
2014). It is classified as a Carcinogenic, Mutagenic and Reprotoxic
(CMR) category 3 due to its toxicity for reproduction.
Because of toluene toxicity, it is necessary to reduce emissions
directly at source. When substitution is not possible, catalytic oxidation
represents an economical and environmental alternative to the thermal
oxidation of VOCs. The choice of suitable catalysts for the total
oxidation of toluene should usually take into account the activity,
stability, cost and feasibility of large scaling-up of laboratory systems.
A catalyst is generally formed by a support and an active surface.
Aluminium oxides, especially α-Al
2
O
3
and γ-Al
2
O
3,
present good
performances as supports for active phases for BTEX oxidation.
Aluminas have some interesting properties like a high thermal stability
for α-Al
2
O
3
or a high specific surface area with acidic properties for γ-
http://dx.doi.org/10.1016/j.envres.2016.10.027
Received 22 July 2016; Received in revised form 24 October 2016; Accepted 27 October 2016
⁎
Corresponding author.
E-mail address: Sylvain.Billet@univ-littoral.fr (S. Billet).
Environmental Research 152 (2017) 328–335
0013-9351/ © 2016 Published by Elsevier Inc.
Available online 09 November 2016
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